Hydroulics calculation and gas properties
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References Inputs Amount fraction Component SG Btu (HHV) T, °F % mol/ mol Btu (LHV) Nitrogen 0.9672 0 60.0 0 0 Car.dio. 1.5195 0 60.0 0 0 Methane 0.5539 891.56 60.0 94.13 802.69 Ethane 1.0382 1562.14 60.0 3.26 1428.84 Propane 1.5225 2221.1 60.0 1.7 2043.37 Iso-butane 1.9373 2879.76 60.0 0.68 2657.6 N-butane 1.9373 2879.76 60.0 0 2657.6 Neo-pentane 2.4911 3538.6 60.0 0.15 3272 Iso-pentane 2.4911 3538.6 60.0 0 3272 N-pentane 2.4911 3538.6 60.0 0 3272 N-hexane 2.9755 4198.24 60.0 0.06 3887.21 Heptane 3.4598 4857.18 60.0 0.02 4501.72 Water 0.6220 44.433 60.0 0 0 Oxygen 1.1048 0 60.0 0 0 100 Wobbe Index MWI SG LHV HHV 52.1899658952771 55.5119221441 0.6005232 979.7 40.4437958 Tb 520 Pb 14.7 F P1 1320.04 P2 1284.38959839 G 0.6 Tf 520 Le 77.6 Z 0.84848 F 16.8609 D 41.055 Q 530930000 Q CALCULATE 530930000 ISO 6976 (1995) Natural gas - Calculation of calorific values, density, relative density and Wobbe
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Hydroulics calculation
Transcript of Hydroulics calculation and gas properties
References
Inputs Amount fraction Superior (gross) calorific Component SG Btu (HHV) T, °F % mol/ mol Btu (LHV) value (MJ/kg)Nitrogen 0.9672 0 60.0 0 0 0Car.dio. 1.5195 0 60.0 0 0 0Methane 0.5539 891.56 60.0 94.13 802.69### 37.706Ethane 1.0382 1562.14 60.0 3.26 1428.84### 66.07Propane 1.5225 2221.1 60.0 1.7 2043.37### 93.94Iso-butane 1.9373 2879.76 60.0 0.68 2657.6### 121.79N-butane 1.9373 2879.76 60.0 0 2657.6### 121.79Neo-pentane 2.4911 3538.6 60.0 0.15 3272### 149.66Iso-pentane 2.4911 3538.6 60.0 0 3272### 149.66N-pentane 2.4911 3538.6 60.0 0 3272### 149.66N-hexane 2.9755 4198.24 60.0 0.06 3887.21### 177.55Heptane 3.4598 4857.18 60.0 0.02 4501.72 205.42Water 0.6220 44.433 60.0 0 0 1.88Oxygen 1.1048 0 60.0 0 0 0
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Wobbe Index MWI SG LHV HHV52.1899658952772 55.51192214406 0.6005232 979.71 40.4437958
Tb 520Pb 14.7 F 0.01407P1 1320.04 0.1186170308P2 1284.389598386G 0.6 1.0002238517Tf 520Le 77.6Z 0.84848F 16.8609D 41.055Q 530930000Q CALCULATE 530930000
ISO 6976 (1995) Natural gas - Calculation of calorific values, density, relative density and Wobbe index from composition
GCV (MJ/m³)
LHV Converter SG max WI min WI max SG min SGNGV(MJ/m³)
0 0 0 0 0 5 0 00 0 0 0 0 3 5 0
35.4926578 911.134 857.65 33.948 0.521406086 83 91.97 83 1002.153882 1621.89 52.874 60.43 0.033846478 10.84 0 5.82 01.59698 2319.44 39.43 86.42 0.025883346 3.15 0 3.15 0
0.828172 3016.71 20.514 112.4 0.013173348 2 0 2 00 3016.71 0 112.4 0 0 0 0 0
0.22449 3714 5.571 138.38 0.003736716 0 0 0 00 3714 0 138.38 0 0 0 0 00 3714 0 138.38 0 0 0 0 0
0.10653 4412.35 2.6474 164.4 0.001785275 0 0 0 00.041084 5109.9 1.022 190.39 0.000691954 1 0 1 0
0 0 0 0 0 0.01 0.01 0.01 00 0 0 0 0 0 0.02 0.02 0
Methane 94.13Ethane 3.26Propane 1.7Butane 0.68Pentane 0.15Hexane 0.06Heptane 0.02
16.8609851909 1.438994611E+07
1.1785780542342 0.848480079
Natural gas - Calculation of calorific values, density, relative density and Wobbe index from composition
GCV (MJ/m³)
SG0.60
47.2 94.99 0.01 5.0048 91.85 3.15 5.0049 93.15 3.00 3.8550 94.70 2.95 2.3551 96.65 2.70 0.65
51.5 96.65 3.15 0.20
WI (MJ/m³)
CH4 C3H8 N2
